US1767886A - Process for bleaching montan wax - Google Patents
Process for bleaching montan wax Download PDFInfo
- Publication number
- US1767886A US1767886A US206799A US20679927A US1767886A US 1767886 A US1767886 A US 1767886A US 206799 A US206799 A US 206799A US 20679927 A US20679927 A US 20679927A US 1767886 A US1767886 A US 1767886A
- Authority
- US
- United States
- Prior art keywords
- wax
- montan wax
- oxidant
- bleaching
- sulfuric acid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000012170 montan wax Substances 0.000 title description 34
- 238000000034 method Methods 0.000 title description 26
- 238000004061 bleaching Methods 0.000 title description 19
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 43
- 239000001993 wax Substances 0.000 description 34
- 239000007800 oxidant agent Substances 0.000 description 26
- 230000001590 oxidative effect Effects 0.000 description 26
- 229940032330 sulfuric acid Drugs 0.000 description 21
- 239000002904 solvent Substances 0.000 description 13
- 239000000470 constituent Substances 0.000 description 12
- 239000007787 solid Substances 0.000 description 12
- 239000002250 absorbent Substances 0.000 description 8
- 230000002745 absorbent Effects 0.000 description 8
- 239000002253 acid Substances 0.000 description 8
- 229910052739 hydrogen Inorganic materials 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 239000003960 organic solvent Substances 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 4
- 150000007513 acids Chemical class 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 4
- KRVSOGSZCMJSLX-UHFFFAOYSA-L chromic acid Substances O[Cr](O)(=O)=O KRVSOGSZCMJSLX-UHFFFAOYSA-L 0.000 description 3
- AWJWCTOOIBYHON-UHFFFAOYSA-N furo[3,4-b]pyrazine-5,7-dione Chemical compound C1=CN=C2C(=O)OC(=O)C2=N1 AWJWCTOOIBYHON-UHFFFAOYSA-N 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 229960000583 acetic acid Drugs 0.000 description 2
- 239000012362 glacial acetic acid Substances 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000000344 soap Substances 0.000 description 2
- MFYSUUPKMDJYPF-UHFFFAOYSA-N 2-[(4-methyl-2-nitrophenyl)diazenyl]-3-oxo-n-phenylbutanamide Chemical compound C=1C=CC=CC=1NC(=O)C(C(=O)C)N=NC1=CC=C(C)C=C1[N+]([O-])=O MFYSUUPKMDJYPF-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004164 Wax ester Substances 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- -1 alkali metal bichromate Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000004203 carnauba wax Substances 0.000 description 1
- 235000013869 carnauba wax Nutrition 0.000 description 1
- 239000002415 cerumenolytic agent Substances 0.000 description 1
- 229940055042 chromic sulfate Drugs 0.000 description 1
- GRWVQDDAKZFPFI-UHFFFAOYSA-H chromium(III) sulfate Chemical compound [Cr+3].[Cr+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O GRWVQDDAKZFPFI-UHFFFAOYSA-H 0.000 description 1
- 229910000356 chromium(III) sulfate Inorganic materials 0.000 description 1
- 239000011696 chromium(III) sulphate Substances 0.000 description 1
- 235000015217 chromium(III) sulphate Nutrition 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- PUZPDOWCWNUUKD-UHFFFAOYSA-M sodium fluoride Chemical compound [F-].[Na+] PUZPDOWCWNUUKD-UHFFFAOYSA-M 0.000 description 1
- 239000002594 sorbent Substances 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
- 239000012178 vegetable wax Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 235000019386 wax ester Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G73/00—Recovery or refining of mineral waxes, e.g. montan wax
Definitions
- This invention relates to the process of bleaching so-called montan wax.
- This mineral in chemical and physicalrespect resembles vegetable waxes, for instance carnauba wax.
- thedark color of the montan wax isagreat draw-back in comparison with vegetable waxes-
- Many attempts have been madeto effect the bleaching of montan wax by physicaland chemical treatment. Upto-date the wax isvdistilled in vacuo with superheated steam whereby a clear product is obtained; however,the output is quite unsatisfactory, and besides the chemical composition of the distillate differs from that of the raw material to a considerable extent. Therefore further trials were made to refine the montan wax solely by chemicalmeans, but the outputs of such methods were likewise very small owing to the extensive formation of resins. I
- montan wax can alsobe bleached by treating it with toxidants such as hydrogen peroxide, chromic acid or an alkali metal bichromate in presence of diluted sulfuric acid.
- toxidants such as hydrogen peroxide, chromic acid or an alkali metal bichromate
- the wax is strongly swelledup and'emulsified in the diluted acid.
- the montan wax offers the oxidants a sur face of attack which otherwise only exists
- the single constituents of the montan wax obtained by fractionating the wax by meansof organic solvents for instance the particularly valuable and easily clearable wax esters, may. be treated according to my present invention, instead of using. the .7 whole or refined montan wax.
- thewax alcohols and acids obtained by saponifying montan wax or the products obtained by transforming these substances may be subjected to the bleaching process.
- the degree of clearing produced by my i r present process depends of course upon the constitution of the raw material, the amount of the oxidant employed and the method fresh. oxidative mixture until the desired I bleaching effectis attained. In this way the oxidant willibe completely utilized and, at thesame time, ahigh bleachingeifectob- 'tained. 1 v
- Rational and uniform oxidation may further be favoured by the addition of inertinorganic or organic distributers.
- solid substances such as silica or, earths, as well as especially inert liquid Wax solvents, for instance carbon tetrachloride, may be used. These solvents are also suitable for checking the thickening phenomena which readily occur during the oxidation.
- the distributers must be removed from the bleached wax by allowing them to set or by filtering or distilling.
- the wax After being treated with diluted sulfuric acid the wax still retains a certain amount of sulfuric acid 'or reduced oxidant. For instance, when employing chromic acid as oxidant, the cleared wax is colored green by a chromic sulfate solution.
- the wax may be treated in the molten'state with diluted acids and finally with water. If required, the'last remnants of coloring contaminations may be removed by treating the wax either molten: or dissolved in a suitable solvent such as benzene, benzine, carbon tetrachloride with small quantities of an absorbent, for instance, floridine, color removing carbon or the like.
- the output of products cleared according to my new process amounts to 88-96%.
- the products retain, their valuable physical properties and are of a light-yellow to white color, which depends upon the amount of the oxidant employed.
- the high fusing point so important for the value is conserved or even increased underthe oxidative treatment provided the oxidation is. not overdone.
- the sulfuric solution of the consumed oxidant obtained by the; present process may he reoxidized in the well-known manner and then re-used.
- the non-sapon V V ifiable part forms a substance yellow as 'wax and'fusing at 77 It may be further cleared up by oxidation as above described. 1
- the dark brown wax acids obtained by decomposing the soaps with mineral acids are converted, according to the foregoing matter from the wax and then treating the,
- Process for bleaching montan wax which comprises treating the wax with an oxidant in presence of moderately diluted sulfuric acid and a distributing medium.
- Process for bleaching montan wax which comprises treating the wa'xWith an oxidant in presence ofmoderately diluted sulfuric acid and washing the product with a diluted acid and thereafter with water.
- Process for bleaching montan wax which comprises treating the Wax with an oxidant in presence of moderately diluted sulfuric acid, dissolving the'product in' the presence of'a decolorizing solid absorbent, separating the solution from'thes'aid solid adsorbent, and removing the solvent em- 5 ployed.
- Process for bleaching montan wax which comprises isolating the constituents of the wax by means of solventd'separately treating the said constituents with an oxidant in presence of moderately diluted sulfuric acid, dissolving the product in an inert organic solvent in the presence of ads colorizing solid absorbent, separating the solution from the said solid absorbenhand removing the solvent employed.
- Process for: bleaching montan wax which comprises treating the waxwith an oxidant in presence of diluted sulfuric acid containing about 65% 'H SO lO.
- Process forbleaching montan wax which comprises extracting the resinous matter from thewaxand then treating the wax with anoxidant in presence of diluted sulfuric acid containing about 65% 'H' S O ioo 11.
- Process for bleaching montan wax which comprises fractionatin the constituents of the wax by means solvents, and separately treating the said constituents with an oxidant in presence of diluted sulfuric acid containing about 65% H 60 12.
- Process for bleaching montan wax which comprises treatingthe wax with a partially exhausted and then with a fresh oxidant in presence of diluted sulfuric acid containing about 65% H SO 13.
- Process for bleaching montan wax which comprises treating the wax with an oxidant in presence of diluted sulfuric acid containing about 65% H SO and a distributing medium.
- Process for bleaching montan wax which comprises treating the wax with an oxidant in presence of diluted sulfuric acid containing about 65% H 80 and washing the product with a diluted acid and thereafter with water; i
- Process for bleaching montan Wax which comprises treating the wax with an oxidant in presence of diluted sulfuric acid containing 65%I-I 'SO dissolving the product in an inert organic solvent in the presence of a decolorizing solid absorbent, separating the solution from the said solid absorbent, and removing the solvent employed.
- Process for bleaching montan wax which comprises fractionating the constituents ofthe wax by means of solvents, separately treating the said constituents with an oxidant in presence of diluted sulfuric acid containing about 65% H SO dissolving the product in an inert organic solvent in the presence of a decolorizing solid absorb- 40 ent, and removing the solvent employed.
- Process for bleaching montan' Wax which comprises treating the wax with an oxidant in presence of diluted sulfuric acid containing about 65% H 80 dissolving the product in the presenceof a decolorizing solid absorbent, separating the solution from the said solid absorbent, and removing the solvent employed.
- Process for bleaching montan wax which comprises fractionating the constituents of the wax by means of solvents, separately treating the said constituents with an oxidant in presence of diluted sulfuric acid containing about H dissolv- 55 ing the product in an inert organic solvent in the presence of a decolorizing solid ab sorbent, separating the solution from the said solid absorbent, and removing the solvent employed. 7 so In testimony whereof I aflix my signature.
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Fats And Perfumes (AREA)
Description
l atent ed June 24, 193(l @UNITED STATES ,PATENTOFFICE mnnonon HELLTH/ALER, oFsnANscHUTz, GERMANY, Assrenon TO THE FIR-M A. RIE- rmx'scmi 'MONTANWERKE AKTIENGESELLSCHAFT,.OF anna, SAALE; GERMANY rnoenss non BLEACI-IING MONTAN wAx No Drawing. Application filed July 18, 1927, Serial No. 206,799, and'in Germany July 26, 1926;
This invention relates to the process of bleaching so-called montan wax. This mineral in chemical and physicalrespect resembles vegetable waxes, for instance carnauba wax. However thedark color of the montan wax isagreat draw-back in comparison with vegetable waxes- Many attempts have been madeto effect the bleaching of montan wax by physicaland chemical treatment. Upto-date the wax isvdistilled in vacuo with superheated steam whereby a clear product is obtained; however,the output is quite unsatisfactory, and besides the chemical composition of the distillate differs from that of the raw material to a considerable extent. Therefore further trials were made to refine the montan wax solely by chemicalmeans, but the outputs of such methods were likewise very small owing to the extensive formation of resins. I
.It has recently been proposed to bleach montan wax by chromic acid in presence of glacial acetic acid. With this oxidant it is possible to obtain a. satisfactoryoutput of a, clear product which substantially conserves the character of the; original wax.
However, the relatively high'price of glacial acetic acid as well as its unpleasant properties prevent a general application of this process which is therefore not carried out on an industrial scale. I
Now I- have found that montan wax can alsobe bleached by treating it with toxidants such as hydrogen peroxide, chromic acid or an alkali metal bichromate in presence of diluted sulfuric acid. When stirring montan wax in the molten state with oxidants in presenceiof diluted acid, the wax is strongly swelledup and'emulsified in the diluted acid. In the state of distribution the montan wax offers the oxidants a sur face of attack which otherwise only exists,
in the state of real solution, Suitable concentrations a'IId'QOIIdltIOIIS of working are described in the examples given at the end:
of the specification However, my invention is not Qconfined' to these conditions which maybe varied within wide limits without departing from the scopeof -my invention.
: After the darkening constituents of the montan wax have been oxidized, the cleared montan wax and the sulfuric acid separate into two distinct layers from which the upper, consisting of wax may easily be re moved. ;v Asthe resinous constituents of .the raw montan wax are violently attacked by the oxidizing agent, whereby less valuable products are formed, it is advisable to separate the resins from the montan wax by any known process before the oxidative' treatment, especially when a montan wax rich in resins is to be treated. The preliminary separation of the resins affords the further advantage of saving oxidizing agents. As a result thethickening phenomena which disturb theuniform action of the oxidizing liquorwand which otherwisecan be avoided only with difficulty arereducedto a mini mum. V t In order to obtain products having special properties,-the single constituents of the montan wax obtained by fractionating the wax by meansof organic solvents, for instance the particularly valuable and easily clearable wax esters, may. be treated according to my present invention, instead of using. the .7 whole or refined montan wax. In the same. manner thewax alcohols and acids obtained by saponifying montan wax or the products obtained by transforming, these substances may be subjected to the bleaching process."
The degree of clearing produced by my i r present process depends of course upon the constitution of the raw material, the amount of the oxidant employed and the method fresh. oxidative mixture until the desired I bleaching effectis attained. In this way the oxidant willibe completely utilized and, at thesame time, ahigh bleachingeifectob- 'tained. 1 v
' Rational and uniform oxidation may further be favoured by the addition of inertinorganic or organic distributers. For this purpose solid substances such as silica or, earths, as well as especially inert liquid Wax solvents, for instance carbon tetrachloride, may be used. These solvents are also suitable for checking the thickening phenomena which readily occur during the oxidation. Of course, the distributers must be removed from the bleached wax by allowing them to set or by filtering or distilling.
After being treated with diluted sulfuric acidthe wax still retains a certain amount of sulfuric acid 'or reduced oxidant. For instance, when employing chromic acid as oxidant, the cleared wax is colored green by a chromic sulfate solution. For further refinement the wax may be treated in the molten'state with diluted acids and finally with water. If required, the'last remnants of coloring contaminations may be removed by treating the wax either molten: or dissolved in a suitable solvent such as benzene, benzine, carbon tetrachloride with small quantities of an absorbent, for instance, floridine, color removing carbon or the like. The output of products cleared according to my new process amounts to 88-96%. The products retain, their valuable physical properties and are of a light-yellow to white color, which depends upon the amount of the oxidant employed. The high fusing point so important for the value is conserved or even increased underthe oxidative treatment provided the oxidation is. not overdone.
' The sulfuric solution of the consumed oxidant obtained by the; present process may he reoxidized in the well-known manner and then re-used.
Exam Zes 1'. 500 gramsof raw black-colored nion tan wax are melted and mlxed with a solution of 1250 grams of concentrated sulfuric acid in 680 grams of water. With continuous stirring a solution of 500 grams of sodiv um bichroinate in 500 grams of waterfis added within lhours. Stirring is continued until'the solution has. become dark green. After stopping the stirrer the oxidized wax rises to the top of the chromic liquor and is removed. After melting and washing with a '10% sulfuric acid and finally with water a yellow wax is obtained, the output amounting to 90%.
2. The same operations as in the foregoing example, but using a montan wax freed from resins in the well-known manner. A
yellow wax is obtained. 7
Raw montan wax'is saponified and the non-saponifiable part removed from the soaps by avolatile solvent. The non-sapon V V ifiable part forms a substance yellow as 'wax and'fusing at 77 It may be further cleared up by oxidation as above described. 1 The dark brown wax acids obtained by decomposing the soaps with mineral acids are converted, according to the foregoing matter from the wax and then treating the,
wax with an oxidant in presenceof mod; erately diluted sulfuricacid.
3. Process for; bleachingmontan wax which comprises isolating the constituents of the wax by means of solvents, and sep arately treating the said cofnstituentswith' an oxidant 111' presence of, moderately diluted sulfuric acid. is
l. Process for bleaching montan wax which comprises treating the wax partially exhausted and then with a fre'shoxidant in presence of moderately diluted sulfuric acid. I
5. Process for bleaching montan wax which comprises treating the wax with an oxidant in presence of moderately diluted sulfuric acid and a distributing medium.
6. Process for bleaching montan wax which comprises treating the wa'xWith an oxidant in presence ofmoderately diluted sulfuric acid and washing the product with a diluted acid and thereafter with water.
7'. Process for bleaching montan wax which comprises treating the Wax with an oxidant in presence of moderately diluted sulfuric acid, dissolving the'product in' the presence of'a decolorizing solid absorbent, separating the solution from'thes'aid solid adsorbent, and removing the solvent em- 5 ployed.
8. Process for bleaching montan wax which comprises isolating the constituents of the wax by means of solventd'separately treating the said constituents with an oxidant in presence of moderately diluted sulfuric acid, dissolving the product in an inert organic solvent in the presence of ads colorizing solid absorbent, separating the solution from the said solid absorbenhand removing the solvent employed.
9. Process for: bleaching montan wax which comprises treating the waxwith an oxidant in presence of diluted sulfuric acid containing about 65% 'H SO lO. Process forbleaching montan wax which comprises extracting the resinous matter from thewaxand then treating the wax with anoxidant in presence of diluted sulfuric acid containing about 65% 'H' S O ioo 11. Process for bleaching montan wax which comprises fractionatin the constituents of the wax by means solvents, and separately treating the said constituents with an oxidant in presence of diluted sulfuric acid containing about 65% H 60 12. Process for bleaching montan wax which comprises treatingthe wax with a partially exhausted and then with a fresh oxidant in presence of diluted sulfuric acid containing about 65% H SO 13. Process for bleaching montan wax which comprises treating the wax with an oxidant in presence of diluted sulfuric acid containing about 65% H SO and a distributing medium.
14. Process for bleaching montan wax which comprises treating the wax with an oxidant in presence of diluted sulfuric acid containing about 65% H 80 and washing the product with a diluted acid and thereafter with water; i
15. Process for bleaching montan Wax which comprises treating the wax with an oxidant in presence of diluted sulfuric acid containing 65%I-I 'SO dissolving the product in an inert organic solvent in the presence of a decolorizing solid absorbent, separating the solution from the said solid absorbent, and removing the solvent employed. s v
16. Process for bleaching montan wax which comprises fractionating the constituents ofthe wax by means of solvents, separately treating the said constituents with an oxidant in presence of diluted sulfuric acid containing about 65% H SO dissolving the product in an inert organic solvent in the presence of a decolorizing solid absorb- 40 ent, and removing the solvent employed.
17. Process for bleaching montan' Wax which comprises treating the wax with an oxidant in presence of diluted sulfuric acid containing about 65% H 80 dissolving the product in the presenceof a decolorizing solid absorbent, separating the solution from the said solid absorbent, and removing the solvent employed.
18. Process for bleaching montan wax which comprises fractionating the constituents of the wax by means of solvents, separately treating the said constituents with an oxidant in presence of diluted sulfuric acid containing about H dissolv- 55 ing the product in an inert organic solvent in the presence of a decolorizing solid ab sorbent, separating the solution from the said solid absorbent, and removing the solvent employed. 7 so In testimony whereof I aflix my signature.
THEODOR HELLTHALER.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE1767886X | 1926-07-26 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1767886A true US1767886A (en) | 1930-06-24 |
Family
ID=7742453
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US206799A Expired - Lifetime US1767886A (en) | 1926-07-26 | 1927-07-18 | Process for bleaching montan wax |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1767886A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2795595A (en) * | 1954-09-30 | 1957-06-11 | Du Pont | Method for bleaching vegetable oils |
| US3004856A (en) * | 1956-03-02 | 1961-10-17 | Hoechst Ag | Process for the bleaching of waxes or other wax-like materials by oxidation and the new compositions of matter thus obtained |
| US3284478A (en) * | 1962-07-06 | 1966-11-08 | Hoechst Ag | Process for the oxidative bleaching of ester waxes |
-
1927
- 1927-07-18 US US206799A patent/US1767886A/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2795595A (en) * | 1954-09-30 | 1957-06-11 | Du Pont | Method for bleaching vegetable oils |
| US3004856A (en) * | 1956-03-02 | 1961-10-17 | Hoechst Ag | Process for the bleaching of waxes or other wax-like materials by oxidation and the new compositions of matter thus obtained |
| US3284478A (en) * | 1962-07-06 | 1966-11-08 | Hoechst Ag | Process for the oxidative bleaching of ester waxes |
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